Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Northport Unit 2 ICR Test Program

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Monday, February 28, 2011 Page 1 of 57
Northport Unit 2 ICR Test Program

Facility Information:

Northport

301 Eatons Neck Road

Northport NY 11768

Contact: Paul Lynch

Phone: 516-545-2564

Fax: 516-545-2582

Email: paul.lynch@us.ngrid.com

Testing Company:

AirNova Inc.

5845 Clayton Avenue

Pennsauken NJ 08109

Contact:Lenny D. Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: lenny@airnova.com

Air Permit Number:

1-4726-00130/00041

Permitted Source ID/Name:

U-00002 Boiler 2

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

This source is a tangential fired external combustion boiler used for electric generation. Rated at 385 MW and can 

fire either #6 residual oil or natural gas. Exhaust gases from the boiler are split between two air heaters then travel 

through individual dual pass Buell electrostatic precipitators. From the ESP exhaust gas is passed through dual 

induced draft fans then enters the stack through dual breechings.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: Enter ARS ID FRS #: Enter FRS ID

SCC / Description 10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Tangential Firing 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Duct near 

stack 

breaching

0 108 124 65.29 12 12 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Duct near % H2O Method 1 - 4 3 180 0

stack 

breaching

Regulation Description Compound Limit Unit

0

Monday, February 28, 2011 Page 2 of 57
Northport Unit 2 ICR Test Program

Duct near Carbon Monoxide Method 10 3 120 0

stack 

breaching

Duct near Formaldehyde Method 0011 3 120 0

stack 

breaching

Duct near 2,3,7,8-TCDD Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,7,8-PeCDD Method 23 3 480 0

stack 

breaching

Duct near OCDD Method 23 3 480 0

stack 

breaching

Duct near 2,3,7,8-TCDF Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,7,8-PeCDF Method 23 3 480 0

stack 

breaching

Duct near 2,3,4,7,8-PeCDF Method 23 3 480 0

stack 

breaching

Duct near 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

stack 

breaching

Duct near OCDF Method 23 3 480 0

stack 

breaching

Duct near Other TCDD Method 23 3 480 0

stack 

breaching

Duct near Other PeCDD Method 23 3 480 0

stack 

breaching

Duct near Other HxCDD Method 23 3 480 0

stack 

breaching

Duct near Other HpCDD Method 23 3 480 0

stack 

breaching

Duct near Other TCDF Method 23 3 480 0

stack 

breaching

Duct near Other PeCDF Method 23 3 480 0

stack 

breaching

Duct near Other HxCDF Method 23 3 480 0

stack 

breaching

Duct near Other HpCDF Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

stack 

breaching

Monday, February 28, 2011 Page 3 of 57
Northport Unit 2 ICR Test Program

Duct near 3,4,4',5-TCB (PCB81) Method 23 3 480 0

stack 

breaching

Duct near 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

stack 

breaching

Duct near 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

stack 

breaching

Duct near 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

stack 

breaching

Duct near 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

stack 

breaching

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Duct near Method 23 3 480 0

stack 

breaching

Duct near 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

stack 

breaching

Duct near 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

stack 

breaching

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Duct near Method 23 3 480 0

stack 

breaching

Total organic compounds 

(TOC) as Propane

Duct near Method 25A 3 120 0

stack 

breaching

Duct near Hydrogen Fluoride Method 26A 3 180 0

stack 

breaching

Duct near Hydrogen Chloride Method 26A 3 180 0

stack 

breaching

Duct near Hydrogen Chloride Method 26 3 180 0

stack 

breaching

Duct near Hydrogen Fluoride Method 26 3 180 0

stack 

breaching

Duct near Filterable PM2.5 OTM - 27/28 3 240 0

stack 

breaching

Inorganic (Aqueous) 

Condensible Part.

Duct near OTM - 27/28 3 240 0

stack 

breaching

Organic Condensible 

Particulate

Duct near OTM - 27/28 3 240 0

stack 

breaching

Duct near Total PM2.5 OTM - 27/28 3 240 0

stack 

breaching

Monday, February 28, 2011 Page 4 of 57
Northport Unit 2 ICR Test Program

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Duct near Filterable Particulate Method 29 3 240 0

stack 

breaching

Duct near Antimony Method 29 3 240 0

stack 

breaching

Duct near Manganese Method 29 3 240 0

stack 

breaching

Duct near Cadmium Method 29 3 240 0

stack 

breaching

Duct near Selenium Method 29 3 240 0

stack 

breaching

Duct near Lead Method 29 3 240 0

stack 

breaching

Duct near Chromium Method 29 3 240 0

stack 

breaching

Duct near Arsenic Method 29 3 240 0

stack 

breaching

Duct near Beryllium Method 29 3 240 0

stack 

breaching

Duct near Nickel Method 29 3 240 0

stack 

breaching

Duct near O2 Method 3A O2 3 480 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 480 0

stack 

breaching

Duct near O2 Method 3A O2 3 120 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 120 0

stack 

breaching

Duct near O2 Method 3A O2 3 240 0

stack 

breaching

Duct near Co2 Method 3A CO2 3 240 0

stack 

breaching

Duct near Filterable Particulate Method 5 3 240 0

stack 

breaching

Duct near Sulfur Dioxide Method 6C 3 180 0

stack 

breaching

Duct near Nitrogen oxides (NOx) Method 7E 3 180 0

stack 

breaching

Monday, February 28, 2011 Page 5 of 57
Northport Unit 2 ICR Test Program

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Selection of sampling location is not in accordance with applicable methods. 3D traverses were conducted in 

accordance with a plan previously approved by Bill Maxwell to verify cyclonic conditions were not present in the 

sampling location utilized during testing.

Monday, February 28, 2011 Page 6 of 57
Northport Unit 2 ICR Test Program

Sampling / Stack Data Results Summary

Location Duct near stack breaching - Method 0011

Average

Run Number NPT2 R1N NPT2 R1S NPT2 R2N

Test Date 6/12/2010 6/12/2010 6/12/2010

Run Start Time 6/12/2010 

7:10:00 AM

6/12/2010 

7:10:00 

AM

6/12/2010 

10:45:00 AM

Run Finish Time 6/12/2010 

9:22:00 AM

6/12/2010 

9:22:00 

AM

6/12/2010 

1:00:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 85.366 83.894 81.699 83.653

Moisture Content of Stack Gas, % 9.84 7.43 9.62 8.963

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 13 12.1 13 12.700

Oxygen, % 5.2 6.1 5.3 5.533

Average Stack Gas Temperature, °F 346.17 353.79 350.29 350.083

Dry Volumetric Flow Rate, dry scfm 331,648.4 336,275.6 328,593.9 332,172.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 538,079.4 536,405.4 535,401.0 536,628.600

Percent Isokinetic of Sampling Rate, % 98.2 109.4 3.3 70.300

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 7 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 0011 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 8 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 9 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 10 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 11 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 12 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Duct near stack breaching - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 13 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 6C 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 28, 2011 Page 14 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 7E 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Duct near stack breaching - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 15 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 28, 2011 Page 16 of 57
Northport Unit 2 ICR Test Program

Emissions Summary

Location: Duct near stack breaching - Method 0011

Compound: Formaldehyde

Average

RunNumber NPT2 R2S NPT2 R1N NPT2 R1S

Mass_mg 0.00638 0.0062 0.0064 0.006

lb/mmBtuO2 2.35E-06 1.96E-06 2.18E-06 0.000

ppm 2.34E-03 2.05E-03 2.16E-03 0.002

ppm@7%O2 2.18E-03 1.81E-03 2.03E-03 0.002

Location: Duct near stack breaching - Method 0011 3

Compound: Formaldehyde

Average

RunNumber NPT2 R2N NPT2 R3N NPT2 R3S

Mass_mg 0.00625 0.00613 0.00608 0.006

lb/mmBtuO2 2.08E-06 2.04E-06 2.15E-06 0.000

ppm 2.16E-03 2.11E-03 2.14E-03 0.002

ppm@7%O2 1.92E-03 1.89E-03 2.00E-03 0.002

Location: Duct near stack breaching - Method 10

Compound: Carbon Monoxide

Average

Run NPT2 R1N NPT2 R1S NPT2 R2N

Elb/hr 8.01E+00 1.39E+00 2.84E+01 12.600

lb/mmBtuO2 5.09E-03 9.61E-04 1.70E-02 0.008

mg/dscm 6.28E+00 1.16E+00 2.21E+01 9.847

Location: Duct near stack breaching - Method 10 3

Compound: Carbon Monoxide

Average

Run NPT2 R2S NPT2 R3N NPT2 R3S

Elb/hr 2.05E+00 1.78E+01 1.46E+00 7.103

lb/mmBtuO2 1.55E-03 1.07E-02 9.43E-04 0.004

mg/dscm 1.63E+00 1.41E+01 1.16E+00 5.630

Location: Duct near stack breaching - Method 23

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.000000002537 0.000000003305 0.000000003305 0.000

lb/mmBtuO2 2.21E-13 3.36E-13 2.80E-13 0.000

ng/dscm 2.73E-04 4.06E-04 3.64E-04 0.000

ng/dscm@7%O2 2.56E-04 3.89E-04 3.24E-04 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.00000000103 0.00000000135 0.00000000135 0.000

lb/mmBtuO2 8.97E-14 1.37E-13 1.14E-13 0.000

ng/dscm 1.11E-04 1.66E-04 1.49E-04 0.000

Monday, February 28, 2011 Page 17 of 57
Northport Unit 2 ICR Test Program

ng/dscm@7%O2 1.04E-04 1.59E-04 1.33E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.000000000707 0.00000000107 0.00000000107 0.000

lb/mmBtuO2 6.16E-14 1.09E-13 9.06E-14 0.000

ng/dscm 7.60E-05 1.31E-04 1.18E-04 0.000

ng/dscm@7%O2 7.14E-05 1.26E-04 1.05E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000712 0.00000000712 0.0000000156 0.000

lb/mmBtuO2 7.23E-13 6.03E-13 1.49E-12 0.000

ng/dscm 8.74E-04 7.85E-04 1.81E-03 0.001

ng/dscm@7%O2 8.38E-04 6.99E-04 1.72E-03 0.001

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.000000133 0.000000133 0.0000001645 0.000

lb/mmBtuO2 1.35E-11 1.13E-11 1.57E-11 0.000

ng/dscm 1.63E-02 1.47E-02 1.91E-02 0.017

ng/dscm@7%O2 1.56E-02 1.31E-02 1.82E-02 0.016

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.000000511 0.000000511 0.000000522 0.000

lb/mmBtuO2 5.19E-11 4.33E-11 4.97E-11 0.000

ng/dscm 6.27E-02 5.63E-02 6.06E-02 0.060

ng/dscm@7%O2 6.01E-02 5.02E-02 5.77E-02 0.056

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000495 0.0000000495 0.0000000607 0.000

lb/mmBtuO2 5.03E-12 4.19E-12 5.78E-12 0.000

ng/dscm 6.08E-03 5.46E-03 7.04E-03 0.006

ng/dscm@7%O2 5.83E-03 4.87E-03 6.70E-03 0.006

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000375 0.0000000375 0.0000000359 0.000

lb/mmBtuO2 3.81E-12 3.18E-12 3.42E-12 0.000

ng/dscm 4.60E-03 4.13E-03 4.17E-03 0.004

ng/dscm@7%O2 4.41E-03 3.68E-03 3.97E-03 0.004

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000161 0.00000161 0.00000149 0.000

Monday, February 28, 2011 Page 18 of 57
Northport Unit 2 ICR Test Program

lb/mmBtuO2 1.63E-10 1.36E-10 1.42E-10 0.000

ng/dscm 1.98E-01 1.77E-01 1.73E-01 0.183

ng/dscm@7%O2 1.90E-01 1.58E-01 1.65E-01 0.171

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000254 0.0000000254 0.0000000309 0.000

lb/mmBtuO2 2.58E-12 2.15E-12 2.94E-12 0.000

ng/dscm 3.12E-03 2.80E-03 3.59E-03 0.003

ng/dscm@7%O2 2.99E-03 2.49E-03 3.42E-03 0.003

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000103 0.00000000103 0.00000000283 0.000

lb/mmBtuO2 1.05E-13 8.72E-14 2.70E-13 0.000

ng/dscm 1.26E-04 1.14E-04 3.28E-04 0.000

ng/dscm@7%O2 1.21E-04 1.02E-04 3.12E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.000000000811 0.000000000811 0.00000000135 0.000

lb/mmBtuO2 8.23E-14 6.87E-14 1.29E-13 0.000

ng/dscm 9.96E-05 8.94E-05 1.57E-04 0.000

ng/dscm@7%O2 9.55E-05 7.97E-05 1.49E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000015 0.0000000015 0.00000000281 0.000

lb/mmBtuO2 1.52E-13 1.27E-13 2.68E-13 0.000

ng/dscm 1.84E-04 1.65E-04 3.26E-04 0.000

ng/dscm@7%O2 1.76E-04 1.47E-04 3.10E-04 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000188 0.00000000188 0.00000000552 0.000

lb/mmBtuO2 1.91E-13 1.59E-13 5.26E-13 0.000

ng/dscm 2.31E-04 2.07E-04 6.41E-04 0.000

ng/dscm@7%O2 2.21E-04 1.84E-04 6.10E-04 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000296 0.00000000296 0.00000000848 0.000

lb/mmBtuO2 3.01E-13 2.51E-13 8.08E-13 0.000

ng/dscm 3.63E-04 3.26E-04 9.84E-04 0.001

ng/dscm@7%O2 3.48E-04 2.90E-04 9.37E-04 0.001

Compound: 3,3',4,4'-TCB (PCB77)

Average

Monday, February 28, 2011 Page 19 of 57
Northport Unit 2 ICR Test Program

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000352 0.0000000352 0.0000000526 0.000

lb/mmBtuO2 3.57E-12 2.98E-12 5.01E-12 0.000

ng/dscm 4.32E-03 3.88E-03 6.10E-03 0.005

ng/dscm@7%O2 4.14E-03 3.46E-03 5.81E-03 0.004

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000034 0.0000000034 0.00000000379 0.000

lb/mmBtuO2 3.45E-13 2.88E-13 3.61E-13 0.000

ng/dscm 4.18E-04 3.75E-04 4.40E-04 0.000

ng/dscm@7%O2 4.01E-04 3.34E-04 4.19E-04 0.000

Compound: OCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000727 0.0000000727 0.0000000511 0.000

lb/mmBtuO2 7.38E-12 6.16E-12 4.87E-12 0.000

ng/dscm 8.93E-03 8.01E-03 5.93E-03 0.008

ng/dscm@7%O2 8.56E-03 7.14E-03 5.65E-03 0.007

Compound: OCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.0000000136 0.0000000136 0.0000000115 0.000

lb/mmBtuO2 1.38E-12 1.15E-12 1.10E-12 0.000

ng/dscm 1.67E-03 1.50E-03 1.33E-03 0.002

ng/dscm@7%O2 1.60E-03 1.34E-03 1.27E-03 0.001

Compound: Other HpCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000642 0.00000000642 0.0000000058 0.000

lb/mmBtuO2 6.52E-13 5.44E-13 5.53E-13 0.000

ng/dscm 7.88E-04 7.08E-04 6.73E-04 0.001

ng/dscm@7%O2 7.55E-04 6.31E-04 6.41E-04 0.001

Compound: Other HpCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000567 0.00000000567 0.00000000438 0.000

lb/mmBtuO2 5.76E-13 4.80E-13 4.17E-13 0.000

ng/dscm 6.96E-04 6.25E-04 5.08E-04 0.001

ng/dscm@7%O2 6.67E-04 5.57E-04 4.84E-04 0.001

Compound: Other HxCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Monday, February 28, 2011 Page 20 of 57
Northport Unit 2 ICR Test Program

Compound: Other HxCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000195 0.00000000195 0.00000000786 0.000

lb/mmBtuO2 1.98E-13 1.65E-13 7.49E-13 0.000

ng/dscm 2.39E-04 2.15E-04 9.12E-04 0.000

ng/dscm@7%O2 2.29E-04 1.92E-04 8.68E-04 0.000

Compound: Other PeCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000175 0.00000000175 0.0000000192 0.000

lb/mmBtuO2 1.78E-13 1.48E-13 1.83E-12 0.000

ng/dscm 2.15E-04 1.93E-04 2.23E-03 0.001

ng/dscm@7%O2 2.06E-04 1.72E-04 2.12E-03 0.001

Compound: Other TCDD

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000809 0.00000000809 0.00000000935 0.000

lb/mmBtuO2 8.21E-13 6.85E-13 8.91E-13 0.000

ng/dscm 9.93E-04 8.92E-04 1.09E-03 0.001

ng/dscm@7%O2 9.52E-04 7.95E-04 1.04E-03 0.001

Compound: Other TCDF

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 0.00000000381 0.00000000381 0.000000035 0.000

lb/mmBtuO2 3.87E-13 3.23E-13 3.34E-12 0.000

ng/dscm 4.68E-04 4.20E-04 4.06E-03 0.002

ng/dscm@7%O2 4.49E-04 3.74E-04 3.87E-03 0.002

Location: Duct near stack breaching - Method 23 3

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.00000000737 0.000000004103 0.0000000106 0.000

lb/mmBtuO2 7.02E-13 3.36E-13 1.03E-12 0.000

ng/dscm 8.55E-04 4.39E-04 1.27E-03 0.001

ng/dscm@7%O2 8.14E-04 3.89E-04 1.19E-03 0.001

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.00000000189 0.00000000171 0.00000000305 0.000

Monday, February 28, 2011 Page 21 of 57
Northport Unit 2 ICR Test Program

lb/mmBtuO2 1.80E-13 1.40E-13 2.97E-13 0.000

ng/dscm 2.19E-04 1.83E-04 3.67E-04 0.000

ng/dscm@7%O2 2.09E-04 1.62E-04 3.45E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.00000000369 0.00000000136 0.0000000102 0.000

lb/mmBtuO2 3.52E-13 1.11E-13 9.93E-13 0.000

ng/dscm 4.28E-04 1.46E-04 1.23E-03 0.001

ng/dscm@7%O2 4.07E-04 1.29E-04 1.16E-03 0.001

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000553 0.0000000163 0.00000000769 0.000

lb/mmBtuO2 4.52E-13 1.59E-12 6.70E-13 0.000

ng/dscm 5.92E-04 1.96E-03 8.27E-04 0.001

ng/dscm@7%O2 5.24E-04 1.84E-03 7.77E-04 0.001

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000001338 0.000000214 0.0000001457 0.000

lb/mmBtuO2 1.09E-11 2.08E-11 1.27E-11 0.000

ng/dscm 1.43E-02 2.57E-02 1.57E-02 0.019

ng/dscm@7%O2 1.27E-02 2.41E-02 1.47E-02 0.017

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000056 0.000000583 0.000000607 0.000

lb/mmBtuO2 4.58E-11 5.68E-11 5.29E-11 0.000

ng/dscm 6.00E-02 7.01E-02 6.53E-02 0.065

ng/dscm@7%O2 5.31E-02 6.58E-02 6.13E-02 0.060

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000508 0.0000000771 0.0000000554 0.000

lb/mmBtuO2 4.15E-12 7.51E-12 4.83E-12 0.000

ng/dscm 5.44E-03 9.27E-03 5.96E-03 0.007

ng/dscm@7%O2 4.82E-03 8.71E-03 5.60E-03 0.006

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000387 0.000000043 0.0000000439 0.000

lb/mmBtuO2 3.16E-12 4.19E-12 3.82E-12 0.000

ng/dscm 4.14E-03 5.17E-03 4.72E-03 0.005

ng/dscm@7%O2 3.67E-03 4.86E-03 4.43E-03 0.004

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

Monday, February 28, 2011 Page 22 of 57
Northport Unit 2 ICR Test Program

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000172 0.00000165 0.00000186 0.000

lb/mmBtuO2 1.41E-10 1.61E-10 1.62E-10 0.000

ng/dscm 1.84E-01 1.98E-01 2.00E-01 0.194

ng/dscm@7%O2 1.63E-01 1.86E-01 1.88E-01 0.179

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000299 0.000000213 0.0000000418 0.000

lb/mmBtuO2 2.45E-12 2.07E-11 3.64E-12 0.000

ng/dscm 3.20E-03 2.56E-02 4.50E-03 0.011

ng/dscm@7%O2 2.83E-03 2.40E-02 4.23E-03 0.010

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000129 0.0000000533 0.000000000751 0.000

lb/mmBtuO2 1.05E-13 5.19E-12 6.54E-14 0.000

ng/dscm 1.38E-04 6.41E-03 8.08E-05 0.002

ng/dscm@7%O2 1.22E-04 6.02E-03 7.59E-05 0.002

Compound: 2,3,7,8-TCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000096 0.00000000143 0.000000000682 0.000

lb/mmBtuO2 7.85E-14 1.39E-13 5.94E-14 0.000

ng/dscm 1.03E-04 1.72E-04 7.33E-05 0.000

ng/dscm@7%O2 9.12E-05 1.62E-04 6.88E-05 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000109 0.0000000126 0.000000000767 0.000

lb/mmBtuO2 8.91E-14 1.23E-12 6.68E-14 0.000

ng/dscm 1.17E-04 1.51E-03 8.25E-05 0.001

ng/dscm@7%O2 1.04E-04 1.42E-03 7.75E-05 0.001

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000364 0.0000000255 0.00000000297 0.000

lb/mmBtuO2 2.98E-13 2.48E-12 2.59E-13 0.000

ng/dscm 3.90E-04 3.06E-03 3.19E-04 0.001

ng/dscm@7%O2 3.45E-04 2.87E-03 3.00E-04 0.001

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000655 0.0000000581 0.00000000733 0.000

lb/mmBtuO2 5.36E-13 5.66E-12 6.39E-13 0.000

ng/dscm 7.01E-04 6.98E-03 7.88E-04 0.003

ng/dscm@7%O2 6.21E-04 6.56E-03 7.40E-04 0.003

Monday, February 28, 2011 Page 23 of 57
Northport Unit 2 ICR Test Program

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000683 0.0000000782 0.000000113 0.000

lb/mmBtuO2 5.59E-12 7.61E-12 9.84E-12 0.000

ng/dscm 7.31E-03 9.40E-03 1.22E-02 0.010

ng/dscm@7%O2 6.47E-03 8.83E-03 1.15E-02 0.009

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000811 0.00000000628 0.00000000897 0.000

lb/mmBtuO2 6.63E-13 6.11E-13 7.81E-13 0.000

ng/dscm 8.69E-04 7.55E-04 9.65E-04 0.001

ng/dscm@7%O2 7.69E-04 7.09E-04 9.06E-04 0.001

Compound: OCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000308 0.0000000284 0.0000000293 0.000

lb/mmBtuO2 2.52E-12 2.76E-12 2.55E-12 0.000

ng/dscm 3.30E-03 3.41E-03 3.15E-03 0.003

ng/dscm@7%O2 2.92E-03 3.20E-03 2.96E-03 0.003

Compound: OCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000697 0.00000000653 0.0000000067 0.000

lb/mmBtuO2 5.70E-13 6.36E-13 5.84E-13 0.000

ng/dscm 7.46E-04 7.85E-04 7.21E-04 0.001

ng/dscm@7%O2 6.60E-04 7.37E-04 6.77E-04 0.001

Compound: Other HpCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000335 0.00000000434 0.00000000327 0.000

lb/mmBtuO2 2.74E-13 4.23E-13 2.85E-13 0.000

ng/dscm 3.59E-04 5.22E-04 3.52E-04 0.000

ng/dscm@7%O2 3.18E-04 4.90E-04 3.31E-04 0.000

Compound: Other HpCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0 0.00000000215 0.00000000225 0.000

lb/mmBtuO2 0.00E+00 2.09E-13 1.96E-13 0.000

ng/dscm 0.00E+00 2.58E-04 2.42E-04 0.000

ng/dscm@7%O2 0.00E+00 2.42E-04 2.27E-04 0.000

Compound: Other HxCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0 0 0.00000000103 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 8.97E-14 0.000

Monday, February 28, 2011 Page 24 of 57
Northport Unit 2 ICR Test Program

ng/dscm 0.00E+00 0.00E+00 1.11E-04 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 1.04E-04 0.000

Compound: Other HxCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.0000000017 0.0000000112 0.00000000284 0.000

lb/mmBtuO2 1.39E-13 1.09E-12 2.47E-13 0.000

ng/dscm 1.82E-04 1.35E-03 3.05E-04 0.001

ng/dscm@7%O2 1.61E-04 1.27E-03 2.86E-04 0.001

Compound: Other PeCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0 0.0000000722 0.00000000546 0.000

lb/mmBtuO2 0.00E+00 7.03E-12 4.76E-13 0.000

ng/dscm 0.00E+00 8.68E-03 5.87E-04 0.003

ng/dscm@7%O2 0.00E+00 8.15E-03 5.51E-04 0.003

Compound: Other TCDD

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000767 0.0000000136 0.00000000634 0.000

lb/mmBtuO2 6.27E-13 1.32E-12 5.52E-13 0.000

ng/dscm 8.21E-04 1.63E-03 6.82E-04 0.001

ng/dscm@7%O2 7.27E-04 1.53E-03 6.41E-04 0.001

Compound: Other TCDF

Average

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N

Mass_mg 0.00000000116 0.000000266 0.0000000105 0.000

lb/mmBtuO2 9.49E-14 2.59E-11 9.15E-13 0.000

ng/dscm 1.24E-04 3.20E-02 1.13E-03 0.011

ng/dscm@7%O2 1.10E-04 3.01E-02 1.06E-03 0.010

Location: Duct near stack breaching - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run NPT2 R1N NPT2 R1S NPT2 R2N

Elb/hr 2.29E-01 2.31E-01 2.26E-01 0.229

gr/dscf 8.06E-05 8.06E-05 8.01E-05 0.000

lb/mmBtuO2 1.41E-04 1.49E-04 1.41E-04 0.000

mg/dscm 1.84E-01 1.84E-01 1.83E-01 0.184

ppm 1.01E-01 1.01E-01 1.00E-01 0.101

ppm@7%O2 8.94E-02 9.49E-02 8.91E-02 0.091

Monday, February 28, 2011 Page 25 of 57
Northport Unit 2 ICR Test Program

Location: Duct near stack breaching - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run NPT2 R2S NPT2 R3N NPT2 R3S

Elb/hr 2.24E-01 6.76E-01 1.30E+00 0.733

gr/dscf 8.01E-05 2.40E-04 4.81E-04 0.000

lb/mmBtuO2 1.48E-04 4.25E-04 8.85E-04 0.000

mg/dscm 1.83E-01 5.50E-01 1.10E+00 0.611

ppm 1.00E-01 3.00E-01 6.00E-01 0.333

ppm@7%O2 9.33E-02 2.69E-01 5.60E-01 0.307

Location: Duct near stack breaching - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.59 0.73 0.7 0.673

Elb/hr 2.13E-01 2.85E-01 2.51E-01 0.250

lb/mmBtuO2 1.32E-04 1.84E-04 1.69E-04 0.000

mg/dscm 1.69E-01 2.25E-01 2.02E-01 0.199

mg/dscm@7%O2 1.54E-01 2.13E-01 1.96E-01 0.188

Compound: Hydrogen Fluoride

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 1.24 2.73 0.82 1.597

Elb/hr 4.47E-01 1.07E+00 2.94E-01 0.604

lb/mmBtuO2 2.78E-04 6.88E-04 1.98E-04 0.000

mg/dscm 3.55E-01 8.43E-01 2.36E-01 0.478

mg/dscm@7%O2 3.23E-01 7.97E-01 2.29E-01 0.450

Location: Duct near stack breaching - Method 26A 3

Compound: Hydrogen Chloride

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 1.03 0.7 0.97 0.900

Elb/hr 3.81E-01 2.55E-01 3.55E-01 0.330

lb/mmBtuO2 2.48E-04 1.66E-04 2.30E-04 0.000

mg/dscm 2.97E-01 2.04E-01 2.78E-01 0.260

mg/dscm@7%O2 2.87E-01 1.93E-01 2.66E-01 0.249

Compound: Hydrogen Fluoride

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.69 0.87 0.6 0.720

Elb/hr 2.55E-01 3.17E-01 2.19E-01 0.264

lb/mmBtuO2 1.66E-04 2.07E-04 1.42E-04 0.000

mg/dscm 1.99E-01 2.53E-01 1.72E-01 0.208

mg/dscm@7%O2 1.92E-01 2.39E-01 1.65E-01 0.199

Location: Duct near stack breaching - Method 29 

Monday, February 28, 2011 Page 26 of 57
Northport Unit 2 ICR Test Program

Compound: Antimony

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.103755 0.112116 0.28819 0.168

Elb/hr 1.81E-02 2.19E-02 5.23E-02 0.031

lb/mmBtuO2 1.10E-05 1.42E-05 3.21E-05 0.000

mg/dscm 1.45E-02 1.75E-02 4.21E-02 0.025

mg/dscm@7%O2 1.28E-02 1.64E-02 3.73E-02 0.022

Compound: Arsenic

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.00684 0.0053 0.0098 0.007

Elb/hr 1.19E-03 1.03E-03 1.78E-03 0.001

lb/mmBtuO2 7.28E-07 6.71E-07 1.09E-06 0.000

mg/dscm 9.53E-04 8.28E-04 1.43E-03 0.001

mg/dscm@7%O2 8.44E-04 7.78E-04 1.27E-03 0.001

Compound: Beryllium

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.000459 0.000297 0.000714 0.000

Elb/hr 8.00E-05 5.80E-05 1.30E-04 0.000

lb/mmBtuO2 4.88E-08 3.76E-08 7.96E-08 0.000

mg/dscm 6.40E-05 4.64E-05 1.04E-04 0.000

mg/dscm@7%O2 5.67E-05 4.36E-05 9.21E-05 0.000

Compound: Cadmium

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.000859 0.000414 0.000692 0.001

Elb/hr 1.50E-04 8.08E-05 1.26E-04 0.000

lb/mmBtuO2 9.14E-08 5.24E-08 7.71E-08 0.000

mg/dscm 1.20E-04 6.47E-05 1.01E-04 0.000

mg/dscm@7%O2 1.06E-04 6.08E-05 8.94E-05 0.000

Compound: Chromium

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.01128 0.007096 0.011099 0.010

Elb/hr 1.97E-03 1.38E-03 2.02E-03 0.002

lb/mmBtuO2 1.20E-06 8.98E-07 1.24E-06 0.000

mg/dscm 1.57E-03 1.11E-03 1.62E-03 0.001

mg/dscm@7%O2 1.39E-03 1.04E-03 1.43E-03 0.001

Compound: Filterable Particulate

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 253.2 156.6 276.2 228.667

Elb/hr 4.41E+01 3.06E+01 5.02E+01 41.633

lb/mmBtuO2 2.69E-02 1.98E-02 3.08E-02 0.026

mg/dscm 3.53E+01 2.45E+01 4.03E+01 33.367

mg/dscm@7%O2 3.13E+01 2.30E+01 3.57E+01 30.000

Monday, February 28, 2011 Page 27 of 57
Northport Unit 2 ICR Test Program

Compound: Lead

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.0116 0.007869 0.014992 0.011

Elb/hr 2.02E-03 1.54E-03 2.72E-03 0.002

lb/mmBtuO2 1.23E-06 9.96E-07 1.67E-06 0.000

mg/dscm 1.62E-03 1.23E-03 2.19E-03 0.002

mg/dscm@7%O2 1.43E-03 1.16E-03 1.94E-03 0.002

Compound: Manganese

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 1.09183 0.87705 1.67833 1.216

Elb/hr 1.90E-01 1.71E-01 3.05E-01 0.222

lb/mmBtuO2 1.16E-04 1.11E-04 1.87E-04 0.000

mg/dscm 1.52E-01 1.37E-01 2.45E-01 0.178

mg/dscm@7%O2 1.35E-01 1.29E-01 2.17E-01 0.160

Compound: Nickel

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 1.2047 0.83617 1.8112 1.284

Elb/hr 2.10E-01 1.63E-01 3.29E-01 0.234

lb/mmBtuO2 1.28E-04 1.06E-04 2.02E-04 0.000

mg/dscm 1.68E-01 1.31E-01 2.64E-01 0.188

mg/dscm@7%O2 1.49E-01 1.23E-01 2.34E-01 0.169

Compound: Selenium

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R2N

Mass_mg 0.00805 0.00742 0.00776 0.008

Elb/hr 1.40E-03 1.45E-03 1.41E-03 0.001

lb/mmBtuO2 8.57E-07 9.39E-07 8.65E-07 0.000

mg/dscm 1.12E-03 1.16E-03 1.13E-03 0.001

mg/dscm@7%O2 9.92E-04 1.09E-03 1.00E-03 0.001

Location: Duct near stack breaching - Method 29 3

Compound: Antimony

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.137203 0.148469 0.128127 0.138

Elb/hr 2.64E-02 2.68E-02 2.48E-02 0.026

lb/mmBtuO2 1.77E-05 1.52E-05 1.53E-05 0.000

mg/dscm 2.19E-02 2.11E-02 2.02E-02 0.021

mg/dscm@7%O2 2.06E-02 1.76E-02 1.78E-02 0.019

Compound: Arsenic

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.00551 0.00696 0.00451 0.006

Elb/hr 1.06E-03 1.25E-03 8.72E-04 0.001

lb/mmBtuO2 7.13E-07 7.11E-07 5.39E-07 0.000

mg/dscm 8.80E-04 9.90E-04 7.10E-04 0.001

Monday, February 28, 2011 Page 28 of 57
Northport Unit 2 ICR Test Program

mg/dscm@7%O2 8.26E-04 8.24E-04 6.25E-04 0.001

Compound: Beryllium

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.000351 0.000524 0.000353 0.000

Elb/hr 6.76E-05 9.44E-05 6.83E-05 0.000

lb/mmBtuO2 4.54E-08 5.35E-08 4.22E-08 0.000

mg/dscm 5.60E-05 7.45E-05 5.56E-05 0.000

mg/dscm@7%O2 5.26E-05 6.20E-05 4.89E-05 0.000

Compound: Cadmium

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.000371 0.000671 0.000329 0.000

Elb/hr 7.15E-05 1.21E-04 6.36E-05 0.000

lb/mmBtuO2 4.80E-08 6.85E-08 3.93E-08 0.000

mg/dscm 5.92E-05 9.54E-05 5.18E-05 0.000

mg/dscm@7%O2 5.56E-05 7.94E-05 4.56E-05 0.000

Compound: Chromium

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.007807 0.001541 0.007174 0.006

Elb/hr 1.50E-03 2.78E-04 1.39E-03 0.001

lb/mmBtuO2 1.01E-06 1.57E-07 8.57E-07 0.000

mg/dscm 1.25E-03 2.19E-04 1.13E-03 0.001

mg/dscm@7%O2 1.17E-03 1.82E-04 9.94E-04 0.001

Compound: Filterable Particulate

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 191.1 262.7 238.2 230.667

Elb/hr 3.68E+01 4.73E+01 4.61E+01 43.400

lb/mmBtuO2 2.47E-02 2.68E-02 2.84E-02 0.027

mg/dscm 3.05E+01 3.74E+01 3.75E+01 35.133

mg/dscm@7%O2 2.86E+01 3.11E+01 3.30E+01 30.900

Compound: Lead

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.008949 0.01327 0.006609 0.010

Elb/hr 1.72E-03 2.39E-03 1.28E-03 0.002

lb/mmBtuO2 1.16E-06 1.36E-06 7.89E-07 0.000

mg/dscm 1.43E-03 1.89E-03 1.04E-03 0.001

mg/dscm@7%O2 1.34E-03 1.57E-03 9.15E-04 0.001

Compound: Manganese

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 1.04843 1.387952 0.899883 1.112

Elb/hr 2.02E-01 2.50E-01 1.74E-01 0.209

lb/mmBtuO2 1.36E-04 1.42E-04 1.07E-04 0.000

mg/dscm 1.67E-01 1.97E-01 1.42E-01 0.169

Monday, February 28, 2011 Page 29 of 57
Northport Unit 2 ICR Test Program

mg/dscm@7%O2 1.57E-01 1.64E-01 1.25E-01 0.149

Compound: Nickel

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 1.05608 1.53845 0.93699 1.177

Elb/hr 2.03E-01 2.77E-01 1.81E-01 0.220

lb/mmBtuO2 1.37E-04 1.57E-04 1.12E-04 0.000

mg/dscm 1.69E-01 2.19E-01 1.47E-01 0.178

mg/dscm@7%O2 1.59E-01 1.82E-01 1.29E-01 0.157

Compound: Selenium

Average

RunNumber NPT2 R2S NPT2 R3N NPT2 R3S

Mass_mg 0.00816 0.00725 0.00586 0.007

Elb/hr 1.57E-03 1.31E-03 1.13E-03 0.001

lb/mmBtuO2 1.06E-06 7.40E-07 7.00E-07 0.000

mg/dscm 1.30E-03 1.03E-03 9.22E-04 0.001

mg/dscm@7%O2 1.22E-03 8.57E-04 8.11E-04 0.001

Location: Duct near stack breaching - Method 6C

Compound: Sulfur Dioxide

Average

Run NPT2 R1N NPT2 R1S NPT2 R2N

Elb/hr 1.02E+03 9.77E+02 1.01E+03 1,002.333

lb/mmBtuO2 6.35E-01 6.31E-01 6.78E-01 0.648

mg/dscm 8.10E+02 7.74E+02 8.09E+02 797.667

mg/dscm@7%O2 7.36E+02 7.32E+02 7.86E+02 751.333

ppm 3.04E+02 2.90E+02 3.04E+02 299.333

ppm@7%O2 2.76E+02 2.74E+02 2.95E+02 281.667

Location: Duct near stack breaching - Method 6C 3

Compound: Sulfur Dioxide

Average

Run NPT2 R2S NPT2 R3N NPT2 R3S

Elb/hr 9.84E+02 1.04E+03 9.84E+02 1,002.667

lb/mmBtuO2 6.40E-01 6.77E-01 6.39E-01 0.652

mg/dscm 7.69E+02 8.31E+02 7.73E+02 791.000

mg/dscm@7%O2 7.42E+02 7.86E+02 7.41E+02 756.333

ppm 2.89E+02 3.12E+02 2.90E+02 297.000

ppm@7%O2 2.79E+02 2.95E+02 2.78E+02 284.000

Location: Duct near stack breaching - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run NPT2 R1N NPT2 R1S NPT2 R2N

Elb/hr 3.10E+02 3.02E+02 3.32E+02 314.667

lb/mmBtuO2 1.93E-01 1.95E-01 2.23E-01 0.204

mg/dscm 2.47E+02 2.39E+02 2.66E+02 250.667

mg/dscm@7%O2 2.24E+02 2.26E+02 2.59E+02 236.333

ppm 1.29E+02 1.25E+02 1.39E+02 131.000

ppm@7%O2 1.17E+02 1.18E+02 1.35E+02 123.333

Monday, February 28, 2011 Page 30 of 57
Northport Unit 2 ICR Test Program

Location: Duct near stack breaching - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run NPT2 R2S NPT2 R3N NPT2 R3S

Elb/hr 3.15E+02 3.24E+02 3.10E+02 316.333

lb/mmBtuO2 2.05E-01 2.11E-01 1.95E-01 0.204

mg/dscm 2.46E+02 2.59E+02 2.36E+02 247.000

mg/dscm@7%O2 2.37E+02 2.45E+02 2.26E+02 236.000

ppm 1.29E+02 1.35E+02 1.24E+02 129.333

ppm@7%O2 1.25E+02 1.28E+02 1.19E+02 124.000

Location: Duct near stack breaching - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R3S

Mass_mg 11.6 5.9 6 7.833

lb/mmBtuO2 2.19E-03 1.27E-03 1.15E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber NPT2 R1N NPT2 R1S NPT2 R3S

Mass_mg 39.4 361.3 29.7 143.467

lb/mmBtuO2 7.44E-03 7.79E-02 5.71E-03 0.030

Compound: Organic Condensible Particulate

Average

RunNumber NPT2 R1N NPT2 R3S NPT2 R3N

Mass_mg 11.6 2.2 56.7 23.500

lb/mmBtuO2 2.19E-03 4.23E-04 9.73E-03 0.004

Compound: Total PM2.5

Average

RunNumber NPT2 R1N NPT2 R3S NPT2 R3N

Mass_mg 62.6 37.9 93.5 64.667

lb/mmBtuO2 1.18E-02 7.29E-03 1.60E-02 0.012

Location: Duct near stack breaching - OTM - 27/28 3

Compound: Filterable PM2.5

Average

RunNumber NPT2 R3N NPT2 R2N NPT2 R2S

Mass_mg 10.9 18.2 6.4 11.833

lb/mmBtuO2 1.87E-03 3.33E-03 1.30E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber NPT2 R3N NPT2 R2N NPT2 R2S

Mass_mg 25.9 7.6 4.2 12.567

lb/mmBtuO2 4.44E-03 1.39E-03 8.52E-04 0.002

Compound: Organic Condensible Particulate

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Monday, February 28, 2011 Page 31 of 57
Northport Unit 2 ICR Test Program

Process Run Data

Mass_mg 10.1 29.3 101.1 46.833

lb/mmBtuO2 2.18E-03 5.36E-03 2.05E-02 0.009

Compound: Total PM2.5

Average

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S

Mass_mg 377.3 55.1 111.7 181.367

lb/mmBtuO2 8.14E-02 1.01E-02 2.27E-02 0.038

Monday, February 28, 2011 Page 32 of 57
Northport Unit 2 ICR Test Program

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 0 Million Btus 0

10 Heat Input 0 Million Btus 0

11 Heat Input 0 Million Btus 0

12 Heat Input 0 Million Btus 0

2 Heat Input 0 Million Btus 0

3 Heat Input 0 Million Btus 0

4 Heat Input 0 Million Btus 0

5 Heat Input 0 Million Btus 0

6 Heat Input 0 Million Btus 0

7 Heat Input 0 Million Btus 0

8 Heat Input 0 Million Btus 0

9 Heat Input 0 Million Btus 0

1 Average Heat Input 0 MMBtu/hr 0

10 Average Heat Input 0 MMBtu/hr 0

11 Average Heat Input 0 MMBtu/hr 0

12 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 0 MMBtu/hr 0

5 Average Heat Input 0 MMBtu/hr 0

6 Average Heat Input 0 MMBtu/hr 0

7 Average Heat Input 0 MMBtu/hr 0

8 Average Heat Input 0 MMBtu/hr 0

9 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

10 Steam Output 0 1000 lb steam/hr 0

11 Steam Output 0 1000 lb steam/hr 0

12 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

5 Steam Output 0 1000 lb steam/hr 0

6 Steam Output 0 1000 lb steam/hr 0

Monday, February 28, 2011 Page 33 of 57
Northport Unit 2 ICR Test Program

7 Steam Output 0 1000 lb steam/hr 0

8 Steam Output 0 1000 lb steam/hr 0

9 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

10 Synfuel Firing Rate 0 0

11 Synfuel Firing Rate 0 0

12 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

4 Synfuel Firing Rate 0 0

5 Synfuel Firing Rate 0 0

6 Synfuel Firing Rate 0 0

7 Synfuel Firing Rate 0 0

8 Synfuel Firing Rate 0 0

9 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

10 Petroleum Coke Firing Rate 0 0

11 Petroleum Coke Firing Rate 0 0

12 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

4 Petroleum Coke Firing Rate 0 0

5 Petroleum Coke Firing Rate 0 0

6 Petroleum Coke Firing Rate 0 0

7 Petroleum Coke Firing Rate 0 0

8 Petroleum Coke Firing Rate 0 0

9 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

10 Coal Gas Firing Rate 0 0

11 Coal Gas Firing Rate 0 0

12 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

4 Coal Gas Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

6 Coal Gas Firing Rate 0 0

Monday, February 28, 2011 Page 34 of 57
Northport Unit 2 ICR Test Program

7 Coal Gas Firing Rate 0 0

8 Coal Gas Firing Rate 0 0

9 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 gpm 0

10 Fuel Oil Firing Rate 0 gpm 0

11 Fuel Oil Firing Rate 0 gpm 0

12 Fuel Oil Firing Rate 0 gpm 0

2 Fuel Oil Firing Rate 0 gpm 0

3 Fuel Oil Firing Rate 0 gpm 0

4 Fuel Oil Firing Rate 0 gpm 0

5 Fuel Oil Firing Rate 0 gpm 0

6 Fuel Oil Firing Rate 0 gpm 0

7 Fuel Oil Firing Rate 0 gpm 0

8 Fuel Oil Firing Rate 0 gpm 0

9 Fuel Oil Firing Rate 0 gpm 0

1 Flue Gas Flow Rate 0 dscfm 0

10 Flue Gas Flow Rate 0 dscfm 0

11 Flue Gas Flow Rate 0 dscfm 0

12 Flue Gas Flow Rate 0 dscfm 0

4 Flue Gas Flow Rate 0 dscfm 0

5 Flue Gas Flow Rate 0 dscfm 0

6 Flue Gas Flow Rate 0 dscfm 0

7 Flue Gas Flow Rate 0 dscfm 0

8 Flue Gas Flow Rate 0 dscfm 0

9 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

10 Pressure Drop Across FGD (if applicable) 0 in H20 0

11 Pressure Drop Across FGD (if applicable) 0 in H20 0

12 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

5 Pressure Drop Across FGD (if applicable) 0 in H20 0

6 Pressure Drop Across FGD (if applicable) 0 in H20 0

7 Pressure Drop Across FGD (if applicable) 0 in H20 0

8 Pressure Drop Across FGD (if applicable) 0 in H20 0

9 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

Monday, February 28, 2011 Page 35 of 57
Northport Unit 2 ICR Test Program

10 FGD Scrubber Liquor pH 0 pH 0

11 FGD Scrubber Liquor pH 0 pH 0

12 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor pH 0 pH 0

6 FGD Scrubber Liquor pH 0 pH 0

7 FGD Scrubber Liquor pH 0 pH 0

8 FGD Scrubber Liquor pH 0 pH 0

9 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

10 FGD Scrubber Liquor Flow Rate 0 gal/min 0

11 FGD Scrubber Liquor Flow Rate 0 gal/min 0

12 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

6 FGD Scrubber Liquor Flow Rate 0 gal/min 0

7 FGD Scrubber Liquor Flow Rate 0 gal/min 0

8 FGD Scrubber Liquor Flow Rate 0 gal/min 0

9 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

10 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

11 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

12 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

8 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

9 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

Monday, February 28, 2011 Page 36 of 57
Northport Unit 2 ICR Test Program

10 Flue Gas Oxygen Content 0 % 0

11 Flue Gas Oxygen Content 0 % 0

12 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Oxygen Content 0 % 0

6 Flue Gas Oxygen Content 0 % 0

7 Flue Gas Oxygen Content 0 % 0

8 Flue Gas Oxygen Content 0 % 0

9 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

10 Flue Gas Carbon Dioxide Content 0 % 0

11 Flue Gas Carbon Dioxide Content 0 % 0

12 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

6 Flue Gas Carbon Dioxide Content 0 % 0

7 Flue Gas Carbon Dioxide Content 0 % 0

8 Flue Gas Carbon Dioxide Content 0 % 0

9 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

10 Flue Gas Moisture Content 0 % 0

11 Flue Gas Moisture Content 0 % 0

12 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

6 Flue Gas Moisture Content 0 % 0

7 Flue Gas Moisture Content 0 % 0

8 Flue Gas Moisture Content 0 % 0

9 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

10 Flue Gas Sampling Point Temperature 0 Deg F 0

11 Flue Gas Sampling Point Temperature 0 Deg F 0

12 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

6 Flue Gas Sampling Point Temperature 0 Deg F 0

Monday, February 28, 2011 Page 37 of 57
Northport Unit 2 ICR Test Program

7 Flue Gas Sampling Point Temperature 0 Deg F 0

8 Flue Gas Sampling Point Temperature 0 Deg F 0

9 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

10 Flue Gas Pressure 0 atm 0

11 Flue Gas Pressure 0 atm 0

12 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

5 Flue Gas Pressure 0 atm 0

6 Flue Gas Pressure 0 atm 0

7 Flue Gas Pressure 0 atm 0

8 Flue Gas Pressure 0 atm 0

9 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

10 Standard Pressure 0 atm 0

11 Standard Pressure 0 atm 0

12 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

6 Standard Pressure 0 atm 0

7 Standard Pressure 0 atm 0

8 Standard Pressure 0 atm 0

9 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

10 Standard Temperature 0 Deg F 0

11 Standard Temperature 0 Deg F 0

12 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

5 Standard Temperature 0 Deg F 0

6 Standard Temperature 0 Deg F 0

7 Standard Temperature 0 Deg F 0

8 Standard Temperature 0 Deg F 0

9 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 MW 0

10 Unit Gross Electrical Output 0 MW 0

11 Unit Gross Electrical Output 0 MW 0

Monday, February 28, 2011 Page 38 of 57
Northport Unit 2 ICR Test Program

APCD Run Data

Process Lab Run Data

12 Unit Gross Electrical Output 0 MW 0

4 Unit Gross Electrical Output 0 MW 0

5 Unit Gross Electrical Output 0 MW 0

6 Unit Gross Electrical Output 0 MW 0

7 Unit Gross Electrical Output 0 MW 0

8 Unit Gross Electrical Output 0 MW 0

9 Unit Gross Electrical Output 0 MW 0

1 Unit Net Electric Generation 0 MWh 0

10 Unit Net Electric Generation 0 MWh 0

11 Unit Net Electric Generation 0 MWh 0

12 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

5 Unit Net Electric Generation 0 MWh 0

6 Unit Net Electric Generation 0 MWh 0

7 Unit Net Electric Generation 0 MWh 0

8 Unit Net Electric Generation 0 MWh 0

9 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 0 0

1 0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

Monday, February 28, 2011 Page 39 of 57
Northport Unit 2 ICR Test Program

Sampling / Stack Data Results Detail

Location Duct near stack breaching - Method 0011

Average

Run Number NPT2 R1N NPT2 R1S NPT2 R2N

Test Date 6/12/2010 6/12/2010 6/12/2010

Run Start Time 6/12/2010 

7:10:00 AM

6/12/2010 

7:10:00 AM

6/12/2010 

10:45:00 AM

Run Finish Time 6/12/2010 

9:22:00 AM

6/12/2010 

9:22:00 AM

6/12/2010 

1:00:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.193 0.18 1.03 0.468

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.03 1.01 1.03 1.023

Barometric Pressure, inches of Mercury 30.13 30.13 30.08 30.113

Average Orifice Meter Differential, inches H2O 1.54 1.32 1.52 1.460

Dry Gas Meter Volume Sampled, cubic feet 83.792 83.792 81.342 82.975

Average Dry Gas Meter Temperature, °F 79.58 78.10 86.38 81.353

Dry Gas Meter Volume Sampled, dscf 85.366 83.894 81.699 83.653

Total Moisture Liquid collected, g 198 143 184.8 175.267

Volume of Water Vapor, standard cubic feet 9.32 6.73 8.70 8.250

Moisture Content of Stack Gas, % 9.84 7.43 9.62 8.963

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9016 0.9257 0.9038 0.910

Carbon Dioxide, % 13 12.1 13 12.700

Oxygen, % 5.2 6.1 5.3 5.533

Carbon Monoxide & Nitrogen, % 81.8 81.8 81.7 81.767

Fuel Factor 1.21 1.22 1.20

Dry Molecular Weight, lb/lb-Mole 30.29 30.18 30.29 30.253

Wet Molecular weight, lb/lb-Mole 29.08 29.28 29.11 29.157

Flue Gas Static Pressure, inches of H2O 15 15 15 15.000

Absolute Flue Gas Pressure, inches of Mercury 31.23 31.23 31.18 31.213

Average Stack Gas Temperature, °F 346.17 353.79 350.29 350.083

Average Velocity Head, inches of H2O 2.0314059127

9512

2.013412070

48913

1.999598036

83317

2.015

Average Stack Gas Velocity, feet/second 96.43 96.13 95.95 96.170

Stack Cross-Sectional Area, square feet 93.000 93.000 93.000 93.000

Dry Volumetric Flow Rate, dry scfm 331,648.4 336,275.6 328,593.9 332,172.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 538,079.4 536,405.4 535,401.0 536,628.600

Percent Isokinetic of Sampling Rate, % 98.2 109.4 3.3 70.300

Percent Excess Air, % 31.7 39.4 32.6 34.567

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 124 124 124

Rectangular Duct Length, inches 108 108 108

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 28, 2011 Page 40 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 0011 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 41 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 42 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 43 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 44 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 45 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 46 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 47 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 48 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 49 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 50 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 51 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 52 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 6C 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 53 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 54 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 7E 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 28, 2011 Page 55 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 56 of 57
Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 28, 2011 Page 57 of 57